CN105823265A - First-kind thermally driven compression-absorption heat pump - Google Patents
First-kind thermally driven compression-absorption heat pump Download PDFInfo
- Publication number
- CN105823265A CN105823265A CN201610243933.2A CN201610243933A CN105823265A CN 105823265 A CN105823265 A CN 105823265A CN 201610243933 A CN201610243933 A CN 201610243933A CN 105823265 A CN105823265 A CN 105823265A
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- generator
- solution
- heat exchanger
- compressor
- connect
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- 238000010521 absorption reaction Methods 0.000 title claims abstract description 37
- 239000006096 absorbing agent Substances 0.000 claims abstract description 207
- 239000003507 refrigerant Substances 0.000 claims abstract description 156
- 239000006200 vaporizer Substances 0.000 claims description 91
- 239000007788 liquid Substances 0.000 claims description 81
- -1 choke valve Substances 0.000 claims description 18
- 230000007928 solubilization Effects 0.000 claims description 8
- 238000005063 solubilization Methods 0.000 claims description 8
- 230000006835 compression Effects 0.000 claims description 4
- 238000007906 compression Methods 0.000 claims description 4
- 230000008020 evaporation Effects 0.000 claims description 4
- 238000001704 evaporation Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 description 23
- 238000010438 heat treatment Methods 0.000 description 15
- 230000036772 blood pressure Effects 0.000 description 6
- 238000005057 refrigeration Methods 0.000 description 5
- 230000007812 deficiency Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 241000208340 Araliaceae Species 0.000 description 1
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 description 1
- 235000003140 Panax quinquefolius Nutrition 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 235000008434 ginseng Nutrition 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B25/00—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
- F25B25/02—Compression-sorption machines, plants, or systems
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Sorption Type Refrigeration Machines (AREA)
Abstract
The invention provides a first-kind thermally driven compression-absorption heat pump, and belongs to the technical field of heat pumps and thermal energy utilization. An absorber communicates with a generator via a solution pump and a solution heat exchanger; the generator communicates with the absorber via the solution heat exchanger; the generator communicates with a condenser by a refrigerant steam channel; the condenser communicates with an evaporator via a cold throttling valve; the evaporator communicates with the absorber by a refrigerant steam channel; the outside communicates with the compressor by a low-temperature thermal medium channel; the compressor communicates with a second compressor by a low-temperature thermal medium channel and via the evaporator; the second compressor communicates with the expansion machine by a low-temperature thermal medium channel and via a high-temperature heat exchanger; the expansion machine communicates with the outside by a low-temperature thermal medium channel; the generator and the high-temperature heat exchanger separately communicate with the outside by high-temperature thermal medium channels; the absorber and the condenser separately communicate with the outside by heated medium channels; and the expansion machine is connected with the compressor and the second compressor and transmits power, so that the first-kind thermally driven compression-absorption heat pump is formed.
Description
Technical field:
The invention belongs to power, refrigeration and technical field of heat pumps.
Background technology:
Cold demand, heat demand and power demand, central with production for human lives common；In reality, people it is frequently necessary to
High temperature heat is utilized to realize refrigeration, heat supply or be converted into power, it is also desirable to utilize power to carry out freezing or utilize power also
Heat supply is carried out in conjunction with low temperature heat energy.During stating purpose in realization, many considerations will be faced or condition will limit, bag
Include the type of the energy, grade and quantity, the type of user's request, grade and quantity, ambient temperature, the class of low-temperature heat medium
Type, the flow process of equipment, structure and manufacturing cost etc..
Heat energy (temperature difference) with absorption heat pump technology as representative utilizes technology, utilize high-temperature hot load drive realize heat supply or
Refrigeration；Being affected by the character of working media (solution and refrigerant medium), high-temperature hot load often cannot rationally, efficiently
It is applied in absorption heat pump flow process, causes its application and range of application by bigger restriction, also cannot give play to absorption
The advantage that formula heat pump techniques refrigerant vapour latent heat is big.
Further, the kind of low-temperature heat source, with or without with the condition such as temperature height, restriction absorption heat pump technology plays a role
Key factor.Such as, the absorption heat pump with lithium bromide water solution as working medium, it is difficult to adapt to the low-temperature heat medium of lower temperature,
This seriously constrains the application of absorption heat pump.
In order to play the technical advantage of absorption heat pump, improve the value of high-temperature hot load, solve the source of low-temperature heat source
And limiting factor, and consider take into account power drive or meet external impetus demand, the present invention proposes to comprise with compressor, expansion
Including the component such as machine and high-temperature heat exchanger, the temperature difference between high temperature heat source and heated medium is effectively utilized or to high temperature
Between thermal source and environment, the temperature difference effectively utilizes, and has the first kind thermal drivers compressing-absorbing type heat pump of comprehensive advantage.
Summary of the invention:
Present invention is primarily intended to provide series first kind thermal drivers compressing-absorbing type heat pump, concrete summary of the invention subitem to illustrate
As follows:
1. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, decompressor and high-temperature heat exchanger are formed；Absorb
Device has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution pipeline through solution heat
Exchanger connects with absorber, and generator also has refrigerant steam channel to connect with condenser, and condenser also has cryogen liquid pipeline warp
Cold choke valve connects with vaporizer, and vaporizer also has refrigerant steam channel to connect with absorber, and there is low-temperature heat medium passage outside
Connecting with compressor, compressor also has low-temperature heat medium passage to connect through vaporizer and the second compressor, and the second compressor also has
Low-temperature heat medium passage connects with decompressor through high-temperature heat exchanger, and decompressor also has low-temperature heat medium passage and ft connection,
Generator and high-temperature heat exchanger have the most respectively high temperature thermal medium passage and ft connection, absorber and condenser have the most respectively by
Heating medium passage and ft connection, decompressor connects compressor and the second compressor and transmits power, forms first kind heat and drives
Dynamic pressure contracting-absorption heat pump；Wherein, or decompressor connects compressor, the second compressor and solution pump and transmits power.
2. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, decompressor, high-temperature heat exchanger and the 3rd compressor
Formed；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution
Pipeline connects with absorber through solution heat exchanger, and generator also has refrigerant steam channel to connect with condenser, and condenser also has
Cryogen liquid pipeline connects with vaporizer through cold choke valve, and vaporizer also has refrigerant steam channel to connect with absorber, and outside has low
Warm passage and the connection of the 3rd compressor, the 3rd compressor also has low-temperature heat medium passage to connect with compressor through vaporizer,
Compressor also has low-temperature heat medium passage to connect through vaporizer and the second compressor, and the second compressor also has low-temperature heat medium passage
Connecting with decompressor through high-temperature heat exchanger, decompressor also has low-temperature heat medium passage and ft connection, generator and high-temperature hot
Exchanger have the most respectively high temperature thermal medium passage and ft connection, absorber and condenser have the most respectively heated medium passage with
Ft connection, decompressor connects compressor, the second compressor and the 3rd compressor and transmits power, forms first kind thermal drivers
Compressing-absorbing type heat pump；Wherein, or decompressor connects compressor, the second compressor, the 3rd compressor and solution pump and transmits
Power.
3. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, decompressor, high-temperature heat exchanger, the 3rd compressor
Formed with the second high-temperature heat exchanger；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump,
Generator also has concentrated solution pipeline to connect with absorber through solution heat exchanger, and generator also has refrigerant steam channel and condenser
Connection, condenser also has cryogen liquid pipeline to connect with vaporizer through cold choke valve, and vaporizer also has refrigerant steam channel and absorption
Device connects, and outside has low-temperature heat medium passage to connect with compressor, and compressor also has low-temperature heat medium passage through vaporizer and the
Two compressor connections, the second compressor also has low-temperature heat medium passage to connect through high-temperature heat exchanger and the 3rd compressor, and the 3rd
Compressor also has low-temperature heat medium passage to connect with decompressor through the second high-temperature heat exchanger, and decompressor also has low-temperature heat medium to lead to
Road and ft connection, generator, high-temperature heat exchanger and the second high-temperature heat exchanger have high temperature thermal medium passage the most respectively with outer
Portion connects, and absorber and condenser have heated medium passage and ft connection the most respectively, decompressor connect compressor, second
Compressor and the 3rd compressor also transmit power, form first kind thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor even
Connect compressor, the second compressor, the 3rd compressor and solution pump and transmit power.
4. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, decompressor, high-temperature heat exchanger, the second decompressor
Formed with the second high-temperature heat exchanger；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump,
Generator also has concentrated solution pipeline to connect with absorber through solution heat exchanger, and generator also has refrigerant steam channel and condenser
Connection, condenser also has cryogen liquid pipeline to connect with vaporizer through cold choke valve, and vaporizer also has refrigerant steam channel and absorption
Device connects, and outside has low-temperature heat medium passage to connect with compressor, and compressor also has low-temperature heat medium passage through vaporizer and the
Two compressor connections, the second compressor also has low-temperature heat medium passage to connect through high-temperature heat exchanger and the second decompressor, and second
Decompressor also has low-temperature heat medium passage to connect with decompressor through the second high-temperature heat exchanger, and decompressor also has low-temperature heat medium to lead to
Road and ft connection, generator, high-temperature heat exchanger and the second high-temperature heat exchanger have high temperature thermal medium passage the most respectively with outer
Portion connects, and absorber and condenser have heated medium passage and ft connection, decompressor and the second decompressor to connect the most respectively
Compressor and the second compressor also transmit power, form first kind thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor and
Second decompressor connects compressor, the second compressor and solution pump and transmits power.
5. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, decompressor, high-temperature heat exchanger and regenerator institute group
Become；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution pipeline
Connecting with absorber through solution heat exchanger, generator also has refrigerant steam channel to connect with condenser, and condenser also has cryogen
Liquid pipeline connects with vaporizer through cold choke valve, and vaporizer also has refrigerant steam channel to connect with absorber, and there is Low Temperature Thermal outside
Medium channel connects with compressor, and compressor also has low-temperature heat medium passage to connect with vaporizer and the second compressor through regenerator,
Second compressor also has low-temperature heat medium passage to connect with decompressor with high-temperature heat exchanger through regenerator, and decompressor also has low temperature
Hot media channel and ft connection, generator and high-temperature heat exchanger have high temperature thermal medium passage and ft connection the most respectively, inhale
Receiving device and condenser has heated medium passage and ft connection the most respectively, decompressor connects compressor and the second compressor and passes
Defeated power, forms first kind thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor connect compressor, the second compressor and
Solution pump also transmits power.
6. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, throttling
Valve, solution pump, solution heat exchanger, compressor, the second compressor, decompressor, high-temperature heat exchanger and regenerator institute group
Become；Absorber has weak solution pipeline to connect with generator with solution heat exchanger through solution pump, and generator also has concentrated solution pipeline
Connecting with absorber through solution heat exchanger, generator also has refrigerant steam channel to connect with condenser, and condenser also has cryogen
Liquid pipeline connects with vaporizer through cold choke valve, and vaporizer also has refrigerant steam channel to connect with absorber, and there is Low Temperature Thermal outside
Medium channel connects with compressor through regenerator, and compressor also has low-temperature heat medium passage to press through vaporizer and regenerator and second
Contracting machine connects, and the second compressor also has low-temperature heat medium passage to connect with decompressor through high-temperature heat exchanger, and decompressor is the lowest
Warm passage and ft connection, generator and high-temperature heat exchanger have high temperature thermal medium passage and ft connection the most respectively,
Absorber and condenser have heated medium passage and ft connection the most respectively, and decompressor connection compressor and the second compressor are also
Transmission power, forms first kind thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor connect compressor, the second compressor
With solution pump transmit power.
7. first kind thermal drivers compressing-absorbing type heat pump, is at the described arbitrary first kind thermal drivers compressing-absorbing type of 1-6 item
Heat pump, increases the second generator, second throttle, the second solution pump and the second solution heat exchanger, and absorber is set up dilute molten
Liquid pipeline is through the second solution pump and the second solution heat exchanger and the connection of the second generator, and the second generator also has concentrated solution pipeline
Connect with absorber through the second solution heat exchanger, generator has refrigerant steam channel connect with condenser and is adjusted to generator
After having refrigerant steam channel to connect with the second generator, the second generator has cryogen liquid pipeline again through second throttle and condenser
Connection, the second generator also has refrigerant steam channel to connect with condenser, forms first kind thermal drivers compressing-absorbing type heat pump.
8. first kind thermal drivers compressing-absorbing type heat pump, is at the described arbitrary first kind thermal drivers compressing-absorbing type of 1-6 item
Heat pump, increases the second generator, second throttle and the second solution heat exchanger, absorber has weak solution pipeline through solution
Pump and solution heat exchanger connect with generator and are adjusted to absorber and have weak solution pipeline through solution pump, solution heat exchanger and
Two solution heat exchangers connect with generator, and generator has concentrated solution pipeline connect adjustment with absorber through solution heat exchanger
Having concentrated solution pipeline to connect through the second solution heat exchanger and the second generator for generator, the second generator has concentrated solution pipe again
Road connects with absorber through solution heat exchanger, generator has refrigerant steam channel connect with condenser and is adjusted to generator and has
After refrigerant steam channel connects with the second generator, the second generator has cryogen liquid pipeline through second throttle with condenser even again
Logical, the second generator also has refrigerant steam channel to connect with condenser, forms first kind thermal drivers compressing-absorbing type heat pump.
9. first kind thermal drivers compressing-absorbing type heat pump, is at the described arbitrary first kind thermal drivers compressing-absorbing type of 1-6 item
Heat pump, increases the second generator, second throttle, the second solution pump and the second solution heat exchanger, is had by absorber dilute molten
Liquid pipeline connects with generator through solution pump and solution heat exchanger and is adjusted to absorber and has weak solution pipeline through solution pump and solution
Heat exchanger and the connection of the second generator, the second generator has concentrated solution pipeline again through the second solution pump and the second solution heat exchange
Device connects with generator, generator has concentrated solution pipeline connect with absorber through solution heat exchanger and is adjusted to generator and has dense
Solution line connects with absorber with solution heat exchanger through the second solution heat exchanger, generator is had refrigerant steam channel with
Condenser connection is adjusted to the second generator after generator has refrigerant steam channel to connect with the second generator cryogen liquid pipe again
Road connects with condenser through second throttle, and the second generator also has refrigerant steam channel to connect with condenser, forms the first kind
Thermal drivers compressing-absorbing type heat pump.
10. first kind thermal drivers compressing-absorbing type heat pump, is in 1-6 item described arbitrary first kind thermal drivers compression-absorption
Formula heat pump, increases the second generator, the second absorber, the second solution pump and the second solution heat exchanger, is had by absorber dilute
Solution line connects with generator through solution pump and solution heat exchanger and is adjusted to absorber and has weak solution pipeline through solution pump and molten
Liquid heat exchanger and the connection of the second absorber, the second absorber has weak solution pipeline to hand over through the second solution pump and the second solution heat again
Parallel operation connects with generator, generator has concentrated solution pipeline connect with absorber through solution heat exchanger and is adjusted to generator and has
Concentrated solution pipeline connects through the second solution heat exchanger and the second generator, and the second generator has concentrated solution pipeline again through solution heat
Exchanger connects with absorber, and the second generator also has refrigerant steam channel to connect with the second absorber, and the second generator also has
High temperature thermal medium passage and ft connection, the second absorber also has heated medium passage and ft connection, forms first kind heat
Drive compression-absorption heat pump.
11. first kind thermal drivers compressing-absorbing type heat pumps, are at the 10th described arbitrary first kind thermal drivers compressing-absorbing type
Heat pump, increases the 3rd generator, second throttle, the 3rd solution pump and the 3rd solution heat exchanger, and the second absorber is set up
Weak solution pipeline is through the 3rd solution pump and the 3rd solution heat exchanger and the connection of the 3rd generator, and the 3rd generator also has concentrated solution
Pipeline connects through the 3rd solution heat exchanger and the second generator, and generator has refrigerant steam channel connect adjustment with condenser
After having refrigerant steam channel to connect with the 3rd generator for generator, the 3rd generator has cryogen liquid pipeline again through second throttle
Connecting with condenser, the 3rd generator also has refrigerant steam channel to connect with condenser, forms first kind thermal drivers compression-absorption
Formula heat pump.
12. first kind thermal drivers compressing-absorbing type heat pumps, are at the 10th described arbitrary first kind thermal drivers compressing-absorbing type
Heat pump, increases the 3rd generator, second throttle and the 3rd solution heat exchanger, the second absorber has weak solution pipeline warp
Second solution pump and the second solution heat exchanger connect with generator and are adjusted to the second absorber and have weak solution pipeline through the second solution
Pump, the second solution heat exchanger and the 3rd solution heat exchanger connect with generator, generator have concentrated solution pipeline through second
Solution heat exchanger and the connection of the second generator are adjusted to generator has concentrated solution pipeline through the 3rd solution heat exchanger and the 3rd
Raw device connection, the 3rd generator has concentrated solution pipeline to connect, by generator through the second solution heat exchanger and the second generator again
There is refrigerant steam channel to connect with condenser and be adjusted to after generator has refrigerant steam channel to connect with the 3rd generator the 3rd
Raw device has cryogen liquid pipeline to connect with condenser through second throttle again, and the 3rd generator also has refrigerant steam channel and condenser
Connection, forms first kind thermal drivers compressing-absorbing type heat pump.
13. first kind thermal drivers compressing-absorbing type heat pumps, are at the 10th described arbitrary first kind thermal drivers compressing-absorbing type
Heat pump, increases the 3rd generator, second throttle, the 3rd solution pump and the 3rd solution heat exchanger, is had by the second absorber
Weak solution pipeline connects with generator through the second solution pump and the second solution heat exchanger and is adjusted to the second absorber and has weak solution pipe
Road the second solution pump and the second solution heat exchanger and the connection of the 3rd generator, the 3rd generator has concentrated solution pipeline again through the
Three solution pumps and the 3rd solution heat exchanger connect with generator, generator have concentrated solution pipeline through the second solution heat exchanger
Connect with the second generator be adjusted to generator have concentrated solution pipeline through the 3rd solution heat exchanger and the second solution heat exchanger with
Second generator connection, generator is had refrigerant steam channel connect with condenser be adjusted to generator have refrigerant steam channel and
After 3rd generator connection, the 3rd generator has cryogen liquid pipeline to connect with condenser through second throttle again, the 3rd generator
Also have refrigerant steam channel to connect with condenser, form first kind thermal drivers compressing-absorbing type heat pump.
14. first kind thermal drivers compressing-absorbing type heat pumps, be 1-6, the compression of 10 described arbitrary first kind thermal drivers-
In absorption heat pump, increase newly-increased generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, will occur
Device has refrigerant steam channel to connect with condenser to be adjusted to generator and have refrigerant steam channel to connect with newly-increased absorber, newly-increased inhales
Receiving device also has weak solution pipeline to connect with newly-increased generator with newly-increased solution heat exchanger through new solubilization liquid pump, and newly-increased generator is also
Having concentrated solution pipeline to connect with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has refrigerant steam channel with cold
Condenser connects, and newly-increased generator also has high temperature thermal medium passage and ft connection, newly-increased absorber to also have heated medium passage
With ft connection, form first kind thermal drivers compressing-absorbing type heat pump.
15. first kind thermal drivers compressing-absorbing type heat pumps, are in 7-9 item described arbitrary first kind thermal drivers compression-absorption
In formula heat pump, the second generator sets up high temperature thermal medium passage and ft connection, forms first kind thermal drivers compressing-absorbing type heat
Pump.
16. first kind thermal drivers compressing-absorbing type heat pumps, are in 11-13 item described arbitrary first kind thermal drivers compression-suction
In receipts formula heat pump, the 3rd generator sets up high temperature thermal medium passage and ft connection, forms first kind thermal drivers compressing-absorbing type
Heat pump.
17. first kind thermal drivers compressing-absorbing type heat pumps, are in 1-16 item described arbitrary first kind thermal drivers compression-absorption
In formula heat pump, increasing engine, engine connects compressor and transmits power to compressor, forms additional external power drive
First kind thermal drivers compressing-absorbing type heat pump.
18. first kind thermal drivers compressing-absorbing type heat pumps, are in 1-16 item described arbitrary first kind thermal drivers compression-absorption
In formula heat pump, increasing working machine, decompressor connects working machine and transmits power to working machine, and being formed to add externally provides power
The first kind thermal drivers compressing-absorbing type heat pump of load.
Accompanying drawing illustrates:
Fig. 1 is based on the 1st kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 2 is based on the 2nd kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 3 is based on the 3rd kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 4 is based on the 4th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 5 is based on the 5th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 6 is based on the 6th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 7 is based on the 7th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 8 is based on the 8th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Fig. 9 is based on the 9th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 10 is based on the 10th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 11 is based on the 11st kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 12 is based on the 12nd kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 13 is based on the 13rd kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 14 is based on the 14th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 15 is based on the 15th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
Figure 16 is based on the 16th kind of principled thermal system figure of first kind thermal drivers compressing-absorbing type heat pump provided by the present invention.
In figure, 1-absorber, 2-generator, 3-condenser, 4-vaporizer, 5-choke valve, 6-solution pump, 7-is molten
Liquid heat exchanger, 8-compressor, 9-the second compressor, 10-decompressor, 11-high-temperature heat exchanger, 12-the 3rd presses
Contracting machine, 13-the second high-temperature heat exchanger, 14-the second decompressor, 15-regenerator, 16-the second generator, 17-
Two choke valves, 18-the second solution pump, 19-the second solution heat exchanger, 20-the second absorber, 21-the 3rd generator,
22-the 3rd solution pump, 23-the 3rd solution heat exchanger, 24-engine, 25-working machine；A-increases generator newly, and B-is new
Increasing absorber, C-new solubilization liquid pump, D-increases solution heat exchanger newly.
Detailed description of the invention:
First be noted that in the statement of structure and flow process, inessential in the case of do not repeat；To obviously
Flow process is not stated.The present invention is described in detail below in conjunction with the accompanying drawings with example.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 1 is achieved in that
(1), in structure, it is mainly handed over by absorber, generator, condenser, vaporizer, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, decompressor and high-temperature heat exchanger are formed；Absorber 1 has weak solution pipeline through molten
Liquid pump 6 connects with generator 2 with solution heat exchanger 7, generator 2 also have concentrated solution pipeline through solution heat exchanger 7 with
Absorber 1 connects, and generator 2 also refrigerant steam channel connects with condenser 3, and condenser 3 also has cryogen liquid pipeline warp
Cold choke valve 5 connects with vaporizer 4, and vaporizer 4 also refrigerant steam channel connects with absorber 1, and there is Low Temperature Thermal outside
Medium channel connects with compressor 8, and compressor 8 also low-temperature heat medium passage connects with the second compressor 9 through vaporizer 4,
Second compressor 9 also low-temperature heat medium passage connects with decompressor 10 through high-temperature heat exchanger 11, and decompressor 10 is the lowest
Warm passage and ft connection, generator 2 and high-temperature heat exchanger 11 have high temperature thermal medium passage to connect with outside the most respectively
Logical, absorber 1 and condenser 3 have heated medium passage and ft connection, decompressor 10 to connect compressor 8 He the most respectively
Second compressor 9 also transmits power.
(2), in flow process, the weak solution of absorber 1 enters generator 2, high temperature thermal medium through solution pump 6 and solution heat exchanger 7
Flow through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour heat release in heated medium；The refrigerant vapour of condenser 3 is put
Heat becomes cryogen liquid in heated medium, and the cryogen liquid stream of condenser 3 enters vaporizer 4 through choke valve 5 throttling, vaporizer 4
Cryogen liquid absorbs heat into refrigerant vapour and provides to absorber 1；Outer low temperature thermal medium enters compressor 8 boosting and heats up, and flows through
Vaporizer 4 heat release, enter the second compressor 9 boosting afterwards and heat up；The low-temperature heat medium of the second compressor 9 discharge flows through
High-temperature heat exchanger 11 also absorbs heat, and enters decompressor 10 blood pressure lowering work done afterwards and externally discharges；The merit of decompressor 10 output carries
Supply compressor 8 and the second compressor 9 are used as power, and form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 2 is achieved in that
(1), in structure, it is mainly handed over by absorber, generator, condenser, vaporizer, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, decompressor, high-temperature heat exchanger and the 3rd compressor are formed；Absorber 1 has dilute
Solution line connects with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 also has concentrated solution pipeline through solution
Heat exchanger 7 connects with absorber 1, and generator 2 also refrigerant steam channel connects with condenser 3, and condenser 3 also has
Cryogen liquid pipeline connects with vaporizer 4 through cold choke valve 5, and vaporizer 4 also refrigerant steam channel connects with absorber 1,
Outside has low-temperature heat medium passage and the 3rd compressor 12 to connect, and the 3rd compressor 12 also has low-temperature heat medium passage through evaporation
Device 4 connects with compressor 8, and compressor 8 also low-temperature heat medium passage connects with the second compressor 9 through vaporizer 4, the
Two compressors 9 also low-temperature heat medium passage connects with decompressor 10 through high-temperature heat exchanger 11, and decompressor 10 also has low temperature
Hot media channel and ft connection, generator 2 and high-temperature heat exchanger 11 have high temperature thermal medium passage and ft connection the most respectively,
Absorber 1 and condenser 3 have heated medium passage and ft connection, decompressor 10 to connect compressor 8, second the most respectively
Compressor 9 and the 3rd compressor 12 also transmit power.
(2), in flow process, the weak solution of absorber 1 enters generator 2, high temperature thermal medium through solution pump 6 and solution heat exchanger 7
Flow through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour heat release in heated medium；The refrigerant vapour of condenser 3 is put
Heat becomes cryogen liquid in heated medium, and the cryogen liquid stream of condenser 3 enters vaporizer 4 through choke valve 5 throttling, vaporizer 4
Cryogen liquid absorbs heat into refrigerant vapour and provides to absorber 1；Outer low temperature thermal medium enters the 3rd compressor 12 boosting and heats up,
Flow through vaporizer 4 heat release, enter compressor 8 boosting afterwards and heat up；The low-temperature heat medium of compressor 8 discharge flows through evaporation
Device 4 heat release, enter the second compressor 9 boosting afterwards and heat up；The low-temperature heat medium of the second compressor 9 discharge flows through high temperature
Heat exchanger 11 also absorbs heat, and enters decompressor 10 blood pressure lowering work done afterwards and externally discharges；The merit of decompressor 10 output is supplied to
Compressor the 8, second compressor 9 and the 3rd compressor 12 are used as power, and form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 3 is achieved in that
(1), in structure, it is mainly handed over by absorber, generator, condenser, vaporizer, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, decompressor, high-temperature heat exchanger, the 3rd compressor and the second high-temperature heat exchanger institute
Composition；Absorber 1 has weak solution pipeline to connect with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 is also
Having concentrated solution pipeline to connect with absorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel and condenser 3
Connection, condenser 3 also cryogen liquid pipeline connects with vaporizer 4 through cold choke valve 5, and vaporizer 4 also has refrigerant vapour to lead to
Road connects with absorber 1, and outside has low-temperature heat medium passage to connect with compressor 8, and compressor 8 also has low-temperature heat medium to lead to
Road connects with the second compressor 9 through vaporizer 4, and the second compressor 9 also has low-temperature heat medium passage through high-temperature heat exchanger 11
Connecting with the 3rd compressor 12, the 3rd compressor 12 also has low-temperature heat medium passage through the second high-temperature heat exchanger 13 and expansion
Machine 10 connects, and decompressor 10 also has low-temperature heat medium passage and ft connection, generator 2, high-temperature heat exchanger 11 and the
Two high-temperature heat exchangers 13 have the most respectively high temperature thermal medium passage and ft connection, absorber 1 and condenser 3 have the most respectively by
Heating medium passage and ft connection, decompressor 10 connects compressor the 8, second compressor 9 and the 3rd compressor 12 and transmits
Power.
(2), in flow process, the weak solution of absorber 1 enters generator 2, high temperature thermal medium through solution pump 6 and solution heat exchanger 7
Flow through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour heat release in heated medium；The refrigerant vapour of condenser 3 is put
Heat becomes cryogen liquid in heated medium, and the cryogen liquid stream of condenser 3 enters vaporizer 4 through choke valve 5 throttling, vaporizer 4
Cryogen liquid absorbs heat into refrigerant vapour and provides to absorber 1；Outer low temperature thermal medium enters compressor 8 boosting and heats up, and flows through
Vaporizer 4 heat release, enter the second compressor 9 boosting afterwards and heat up；The low-temperature heat medium of the second compressor 9 discharge flows through
High-temperature heat exchanger 11 also absorbs heat, and enters the 3rd compressor 12 boosting afterwards and heats up；The Low Temperature Thermal of the 3rd compressor 12 discharge
Medium flows through the second high-temperature heat exchanger 13 and absorbs heat, and enters decompressor 10 blood pressure lowering work done afterwards and externally discharges；Decompressor
The merit of 10 outputs is supplied to compressor the 8, second compressor 9 and the 3rd compressor 12 is used as power, and forms first kind thermal drivers pressure
Contracting-absorption heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 4 is achieved in that
(1), in structure, it is mainly handed over by absorber, generator, condenser, vaporizer, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, decompressor, high-temperature heat exchanger, the second high-temperature heat exchanger and the second decompressor institute
Composition；Absorber 1 has weak solution pipeline to connect with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 is also
Having concentrated solution pipeline to connect with absorber 1 through solution heat exchanger 7, generator 2 also has refrigerant steam channel and condenser 3
Connection, condenser 3 also cryogen liquid pipeline connects with vaporizer 4 through cold choke valve 5, and vaporizer 4 also has refrigerant vapour to lead to
Road connects with absorber 1, and outside has low-temperature heat medium passage to connect with compressor 8, and compressor 8 also has low-temperature heat medium to lead to
Road connects with the second compressor 9 through vaporizer 4, and the second compressor 9 also has low-temperature heat medium passage through high-temperature heat exchanger 11
Connecting with the second decompressor 14, the second decompressor 14 also has low-temperature heat medium passage through the second high-temperature heat exchanger 13 and expansion
Machine 10 connects, and decompressor 10 also has low-temperature heat medium passage and ft connection, generator 2, high-temperature heat exchanger 11 and the
Two high-temperature heat exchangers 13 have the most respectively high temperature thermal medium passage and ft connection, absorber 1 and condenser 3 have the most respectively by
Heating medium passage and ft connection, decompressor 10 and the second decompressor 14 connect compressor 8 and the second compressor 9 and pass
Defeated power.
(2), in flow process, the weak solution of absorber 1 enters generator 2, high temperature thermal medium through solution pump 6 and solution heat exchanger 7
Flow through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour heat release in heated medium；The refrigerant vapour of condenser 3 is put
Heat becomes cryogen liquid in heated medium, and the cryogen liquid stream of condenser 3 enters vaporizer 4 through choke valve 5 throttling, vaporizer 4
Cryogen liquid absorbs heat into refrigerant vapour and provides to absorber 1；Outer low temperature thermal medium enters compressor 8 boosting and heats up, and flows through
Vaporizer 4 heat release, enter the second compressor 9 boosting afterwards and heat up；The low-temperature heat medium of the second compressor 9 discharge flows through
High-temperature heat exchanger 11 also absorbs heat, and enters the second decompressor 14 blood pressure lowering work done afterwards；The Low Temperature Thermal of the second decompressor 14 discharge
Medium flows through the second high-temperature heat exchanger 13 and absorbs heat, and enters decompressor 10 blood pressure lowering work done afterwards and externally discharges；Decompressor
10 and second the merit of decompressor 14 output be supplied to compressor 8 and the second compressor 9 is used as power, form first kind thermal drivers pressure
Contracting-absorption heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 5 is achieved in that
(1), in structure, it is mainly handed over by absorber, generator, condenser, vaporizer, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, decompressor, high-temperature heat exchanger and regenerator are formed；Absorber 1 has weak solution
Pipeline connects with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 also has concentrated solution pipeline to hand over through solution heat
Parallel operation 7 connects with absorber 1, and generator 2 also refrigerant steam channel connects with condenser 3, and condenser 3 also has cryogen
Liquid pipeline connects with vaporizer 4 through cold choke valve 5, and vaporizer 4 also refrigerant steam channel connects with absorber 1, outside
Having low-temperature heat medium passage to connect with compressor 8, compressor 8 also has low-temperature heat medium passage through regenerator 15 and vaporizer 4
Connecting with the second compressor 9, the second compressor 9 also has low-temperature heat medium passage through regenerator 15 and high-temperature heat exchanger 11
Connecting with decompressor 10, decompressor 10 also has low-temperature heat medium passage and ft connection, generator 2 and high-temperature heat exchanger
11 have the most respectively high temperature thermal medium passage and ft connection, absorber 1 and condenser 3 have the most respectively heated medium passage with
Ft connection, decompressor 10 connects compressor 8 and the second compressor 9 and transmits power.
(2), in flow process, the weak solution of absorber 1 enters generator 2, high temperature thermal medium through solution pump 6 and solution heat exchanger 7
Flow through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour heat release in heated medium；The refrigerant vapour of condenser 3 is put
Heat becomes cryogen liquid in heated medium, and the cryogen liquid stream of condenser 3 enters vaporizer 4 through choke valve 5 throttling, vaporizer 4
Cryogen liquid absorbs heat into refrigerant vapour and provides to absorber 1；Outer low temperature thermal medium enters compressor 8 boosting and heats up, successively
Flow through regenerator 15 and vaporizer 4 progressively heat release, enter the second compressor 9 boosting afterwards and heat up；Second compressor 9 row
The low-temperature heat medium put flows through regenerator 15 and high-temperature heat exchanger 11 successively and progressively absorbs heat, and enters decompressor 10 afterwards and drops
Pressure work done is also externally discharged；The merit of decompressor 10 output is supplied to compressor 8 and the second compressor 9 is used as power, and forms first
Class thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 6 is achieved in that
(1), in structure, it is mainly handed over by absorber, generator, condenser, vaporizer, choke valve, solution pump, solution heat
Parallel operation, compressor, the second compressor, decompressor, high-temperature heat exchanger and regenerator are formed；Absorber 1 has weak solution
Pipeline connects with generator 2 with solution heat exchanger 7 through solution pump 6, and generator 2 also has concentrated solution pipeline to hand over through solution heat
Parallel operation 7 connects with absorber 1, and generator 2 also refrigerant steam channel connects with condenser 3, and condenser 3 also has cryogen
Liquid pipeline connects with vaporizer 4 through cold choke valve 5, and vaporizer 4 also refrigerant steam channel connects with absorber 1, outside
Having low-temperature heat medium passage to connect with compressor 8 through regenerator 15, compressor 8 also has low-temperature heat medium passage through vaporizer 4
Connecting with the second compressor 9 with regenerator 15, the second compressor 9 also has low-temperature heat medium passage through high-temperature heat exchanger 11
Connecting with decompressor 10, decompressor 10 also has low-temperature heat medium passage and ft connection, generator 2 and high-temperature heat exchanger
11 have the most respectively high temperature thermal medium passage and ft connection, absorber 1 and condenser 3 have the most respectively heated medium passage with
Ft connection, decompressor 10 connects compressor 8 and the second compressor 9 and transmits power.
(2), in flow process, the weak solution of absorber 1 enters generator 2, high temperature thermal medium through solution pump 6 and solution heat exchanger 7
Flow through generator 2, heating enters its interior solution release refrigerant vapour and provides to condenser 3, the concentrated solution warp of generator 2
Solution heat exchanger 7 enters absorber 1, absorbs refrigerant vapour heat release in heated medium；The refrigerant vapour of condenser 3 is put
Heat becomes cryogen liquid in heated medium, and the cryogen liquid stream of condenser 3 enters vaporizer 4 through choke valve 5 throttling, vaporizer 4
Cryogen liquid absorbs heat into refrigerant vapour and provides to absorber 1；Outer low temperature thermal medium flows through regenerator 15 and absorbs heat, laggard
Enter compressor 8 boosting to heat up；The low-temperature heat medium of compressor 8 discharge flows through vaporizer 4 and regenerator 15 successively and progressively puts
Heat, enters the second compressor 9 boosting afterwards and heats up；The low-temperature heat medium of the second compressor 9 discharge flows through high-temperature heat exchanger
11 and absorb heat, enter decompressor 10 blood pressure lowering work done afterwards and also externally discharge；The merit of decompressor 10 output is supplied to compressor 8
It is used as power with the second compressor 9, forms first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 7 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, the second generator, the second throttling are increased
Valve, the second solution pump and the second solution heat exchanger, it is molten through the second solution pump 18 and second that absorber 1 sets up weak solution pipeline
Liquid heat exchanger 19 connects with the second generator 16, and the second generator 16 also has concentrated solution pipeline through the second solution heat exchanger
19 connect with absorber 1, generator 2 has refrigerant steam channel connect with condenser 3 and is adjusted to generator 2 and has cryogen to steam
After vapour passage and the connection of the second generator 16, the second generator 16 has cryogen liquid pipeline again through second throttle 17 and condenser
3 connections, the second generator 16 also refrigerant steam channel connects with condenser 4.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the second generator 16 and makees to drive thermal medium, absorber 1
Part weak solution enters the second generator 16 through the second solution pump 18 and the second solution heat exchanger 19, and refrigerant vapour flows through
Two generators 16, heating enter its interior solution release refrigerant vapour and also provide to condenser 3, the second generator 16 dense molten
Liquid enters absorber 1 through the second solution heat exchanger 19, flows through after the refrigerant vapour heat release of the second generator 16 becomes cryogen liquid
Enter condenser 3 through second throttle 17 throttling, form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 8 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, the second generator, the second throttling are increased
Valve and the second solution heat exchanger, have weak solution pipeline through solution pump 6 and solution heat exchanger 7 and generator 2 by absorber 1
Connection be adjusted to absorber 1 have weak solution pipeline through solution pump 6, solution heat exchanger 7 and the second solution heat exchanger 19 with
Generator 2 connects, and generator 2 has concentrated solution pipeline connect with absorber 1 through solution heat exchanger 7 and is adjusted to generator 2
Having concentrated solution pipeline to connect with the second generator 16 through the second solution heat exchanger 19, the second generator 16 has concentrated solution pipe again
Road connects with absorber 1 through solution heat exchanger 7, generator 2 has refrigerant steam channel connect with condenser 3 and is adjusted to
After generator 2 has refrigerant steam channel to connect with the second generator 16, the second generator 16 has cryogen liquid pipeline again through second
Choke valve 17 connects with condenser 3, and the second generator 16 also refrigerant steam channel connects with condenser 3.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the second generator 16 and makees to drive thermal medium, absorber 1
Weak solution enters generator 2 through solution pump 6, solution heat exchanger 7 and the second solution heat exchanger 19, generator 2 dense
Solution enters the second generator 16 through the second solution heat exchanger 19, and refrigerant vapour flows through the second generator 16, heating enters
Its interior solution release refrigerant vapour also provides to condenser 3, and the concentrated solution of the second generator 16 is entered through solution heat exchanger 7
Enter absorber 1, flow through after the refrigerant vapour heat release of the second generator 16 becomes cryogen liquid and enter cold through second throttle 17 throttling
Condenser 3, forms first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Fig. 9 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, the second generator, the second throttling are increased
Valve, the second solution pump and the second solution heat exchanger, have weak solution pipeline through solution pump 6 and solution heat exchange by absorber 1
Device 7 connects with generator 2 and is adjusted to absorber 1 and has weak solution pipeline through solution pump 6 and solution heat exchanger 7 and second
Raw device 16 connects, the second generator 16 have again concentrated solution pipeline through the second solution pump 18 and the second solution heat exchanger 19 with
Generator 2 connects, and generator 2 has concentrated solution pipeline connect with absorber 1 through solution heat exchanger 7 and is adjusted to generator 2
There is concentrated solution pipeline to connect with absorber 1 with solution heat exchanger 7 through the second solution heat exchanger 19, generator 2 is had cold
Agent steam channel connects with condenser 3 and is adjusted to after generator 2 has refrigerant steam channel to connect with the second generator 16 second
Generator 16 has cryogen liquid pipeline to connect with condenser 3 through second throttle 17 again, and the second generator 16 also has refrigerant vapour
Passage connects with condenser 3.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the second generator 16 and makees to drive thermal medium, absorber 1
Weak solution enters the second generator 16 through solution pump 6 and solution heat exchanger 7, and refrigerant vapour flows through the second generator 16, adds
Heat enters its interior solution release refrigerant vapour and provides to condenser 3, and the concentrated solution of the second generator 16 is through the second solution pump
18 and second solution heat exchanger 19 enter generator 2, the concentrated solution of generator 2 is through the second solution heat exchanger 19 and molten
Liquid heat exchanger 7 enters absorber 1, flows through the refrigerant vapour heat release of the second generator 16 and becomes after cryogen liquid through second section stream
Valve 17 throttling enters condenser 3, forms first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 10 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, the second generator, the second absorption are increased
Device, the second solution pump and the second solution heat exchanger, have weak solution pipeline through solution pump 6 and solution heat exchange by absorber 1
Device 7 connects with generator 2 and is adjusted to absorber 1 and has weak solution pipeline to inhale through solution pump 6 and solution heat exchanger 7 and second
Receive device 20 to connect, the second absorber 20 have again weak solution pipeline through the second solution pump 18 and the second solution heat exchanger 19 with
Generator 2 connects, and generator 2 has concentrated solution pipeline connect with absorber 1 through solution heat exchanger 7 and is adjusted to generator 2
Having concentrated solution pipeline to connect with the second generator 16 through the second solution heat exchanger 19, the second generator 16 has concentrated solution pipe again
Road connects with absorber 1 through solution heat exchanger 7, and the second generator 16 also has refrigerant steam channel and the second absorber 20
Connection, the second generator 16 also has high temperature thermal medium passage and ft connection, the second absorber 20 to also have heated medium to lead to
Road and ft connection.
(2), in flow process, the weak solution of absorber 1 enters the second absorber 20 through solution pump 6 and solution heat exchanger 7, absorbs
Refrigerant vapour heat release are handed over through the second solution pump 18 and the second solution heat in heated medium, the weak solution of the second absorber 20
Parallel operation 19 enters generator 2, and the concentrated solution of generator 2 enters the second generator 16 through the second solution heat exchanger 19, high
Warm flows through the second generator 16, heating enters its interior solution release refrigerant vapour and provides to the second absorber 20,
The concentrated solution of the second generator 16 enters absorber 1 through solution heat exchanger 7, forms first kind thermal drivers compressing-absorbing type heat
Pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 11 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Figure 10, the 3rd generator, second section are increased
Stream valve, the 3rd solution pump and the 3rd solution heat exchanger, the second absorber 20 sets up weak solution pipeline through the 3rd solution pump 22
Connecting with the 3rd generator 21 with the 3rd solution heat exchanger 23, the 3rd generator 21 also has concentrated solution pipeline through the 3rd solution
Heat exchanger 23 connects with the second generator 16, generator 2 is had refrigerant steam channel connect with condenser 3 be adjusted to send out
After raw device 2 has refrigerant steam channel to connect with the 3rd generator 21, the 3rd generator 21 has cryogen liquid pipeline again through second section
Stream valve 17 connects with condenser 3, and the 3rd generator 21 also refrigerant steam channel connects with condenser 3.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the 3rd generator 21 and makees to drive thermal medium, the second absorber
The part weak solution of 20 enters the 3rd generator 21, refrigerant vapour stream through the 3rd solution pump 22 and the 3rd solution heat exchanger 23
Enter its interior solution release refrigerant vapour through the 3rd generator 21, heating and provide to condenser 3, the 3rd generator 21
Concentrated solution enters the second generator 16 through the 3rd solution heat exchanger 23, and the refrigerant vapour heat release flowing through the 3rd generator 21 becomes
Enter condenser 3 through second throttle 17 throttling after cryogen liquid, form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 12 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Figure 10, the 3rd generator, second section are increased
Stream valve and the 3rd solution heat exchanger, have weak solution pipeline through the second solution pump 18 and the second solution heat by the second absorber 20
Exchanger 19 connects with generator 2 and is adjusted to the second absorber 20 and has weak solution pipeline through second solution pump the 18, second solution
Heat exchanger 19 connects with generator 2 with the 3rd solution heat exchanger 23, has concentrated solution pipeline molten through second in generator 2
Liquid heat exchanger 19 connects with the second generator 16 and is adjusted to generator 2 and has concentrated solution pipeline through the 3rd solution heat exchanger 23
Connecting with the 3rd generator 21, the 3rd generator 21 has concentrated solution pipeline to occur through the second solution heat exchanger 19 and second again
Device 16 connects, generator 2 is had refrigerant steam channel connect with condenser 3 be adjusted to generator 2 have refrigerant steam channel with
After 3rd generator 21 connection, the 3rd generator 21 has cryogen liquid pipeline to connect with condenser 3 through second throttle 17 again,
3rd generator 21 also refrigerant steam channel connects with condenser 3, the 3rd generator 21 also have high temperature thermal medium passage with
Ft connection.
(2), in flow process, the refrigerant vapour that external high temperature thermal medium and generator 2 produce is supplied to the 3rd generator 21 and makees to drive heat
Medium, the weak solution of the second absorber 20 is through the second solution pump the 18, second solution heat exchanger 19 and the 3rd solution heat exchange
Device 23 enters generator 2, and the concentrated solution of generator 2 enters the 3rd generator 21, cryogen through the 3rd solution heat exchanger 23
Steam and high temperature thermal medium flow separately through the 3rd generator 21, heating enters its interior solution and discharges refrigerant vapour and to condenser
3 provide, and the concentrated solution of the 3rd generator 21 enters the second generator 16 through the second solution heat exchanger 19, flows through the 3rd
The refrigerant vapour heat release of raw device 21 enters condenser 3 through second throttle 17 throttling after becoming cryogen liquid, forms first kind heat and drives
Dynamic pressure contracting-absorption heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 13 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Figure 10, the 3rd generator, second section are increased
Stream valve, the 3rd solution pump and the 3rd solution heat exchanger, have weak solution pipeline through the second solution pump 18 by the second absorber 20
Connect with generator 2 with the second solution heat exchanger 19 and be adjusted to the second absorber 20 and have weak solution pipeline through the second solution pump
18 connect with the 3rd generator 21 with the second solution heat exchanger 19, and the 3rd generator 21 has concentrated solution pipeline molten through the 3rd again
Liquid pump 22 connects with generator 2 with the 3rd solution heat exchanger 23, generator 2 has concentrated solution pipeline through the second solution heat
Exchanger 19 connects with the second generator 16 and is adjusted to generator 2 and has concentrated solution pipeline through the 3rd solution heat exchanger 23 and
Two solution heat exchangers 19 connect with the second generator 16, have refrigerant steam channel to connect tune with condenser 3 in generator 2
Whole have refrigerant steam channel to connect with the 3rd generator 21 for generator 2 after the 3rd generator 21 have cryogen liquid pipeline warp again
Second throttle 17 connects with condenser 3, and the 3rd generator 21 also refrigerant steam channel connects with condenser 3.
(2), in flow process, the refrigerant vapour that generator 2 produces is supplied to the 3rd generator 21 and makees to drive thermal medium, the second absorber
The weak solution of 20 enters the 3rd generator 21 through the second solution pump 18 and the second solution heat exchanger 19, and refrigerant vapour flows through
Three generators 21, heating enter its interior solution release refrigerant vapour and also provide to condenser 3, the 3rd generator 21 dense molten
Liquid enters generator 2 through the 3rd solution pump 22 and the 3rd solution heat exchanger 23, and the concentrated solution of generator 2 is through the 3rd solution heat
Exchanger 23 and the second solution heat exchanger 19 enter the second generator 16, flow through the refrigerant vapour heat release of the 3rd generator 21
Enter condenser 3 through second throttle 17 throttling after becoming cryogen liquid, form first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 14 is achieved in that
(1) in structure, in the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, newly-increased generator, newly-increased absorption are increased
Device, new solubilization liquid pump and newly-increased solution heat exchanger, have generator 2 refrigerant steam channel to connect with condenser 3 and be adjusted to
Generator 2 has refrigerant steam channel to connect with newly-increased absorber B, and newly-increased absorber B also has weak solution pipeline through new solubilization liquid
Pump C connects with newly-increased generator A with newly-increased solution heat exchanger D, and newly-increased generator A also has concentrated solution pipeline through new solubilising
Liquid heat exchanger D connects with newly-increased absorber B, and newly-increased generator A also has refrigerant steam channel to connect with condenser 3, newly
Increasing generator A and also have high temperature thermal medium passage and ft connection, newly-increased absorber B also has heated medium passage to connect with outside
Logical.
(2), in flow process, the refrigerant vapour that generator 2 produces enters newly-increased absorber B, and the weak solution of newly-increased absorber B is through newly-increased
Solution pump C and newly-increased solution heat exchanger D enter newly-increased generator A, high temperature thermal medium flow through newly-increased generator A, heat into
Entering its interior solution release refrigerant vapour and provide to condenser 3, the concentrated solution of newly-increased generator A is through new solubilization liquid heat exchange
Device D enters newly-increased absorber B, absorbs refrigerant vapour heat release in heated medium, formation first kind thermal drivers compression-absorb
Formula heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 15 is achieved in that
In the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, increasing engine, engine 24 connects compressor 8
And transmit power to compressor 8, form additional external power-actuated first kind thermal drivers compressing-absorbing type heat pump.
First kind thermal drivers compressing-absorbing type heat pump shown in Figure 16 is achieved in that
In the compressing-absorbing type heat pump of first kind thermal drivers shown in Fig. 1, increasing working machine, decompressor 10 connects working machine 25
And transmit power to working machine 25, form the additional first kind thermal drivers compressing-absorbing type heat pump that living load is externally provided.
The first kind thermal drivers compressing-absorbing type heat pump that effect that the technology of the present invention can realize is proposed by the invention, has
Following effect and advantage:
(1) new approaches and new technique that the temperature difference utilizes are proposed.
(2) heat energy (temperature difference) drives, it is achieved heat supply/refrigeration, or externally provides power while of optional.
(3) flow process is reasonable, and performance index is variable and corresponding with thermodynamic parameter change, it is possible to realize filling of heat energy (temperature difference)
Divide and efficiently utilize.
(4) if desired, realizing heat supply/refrigeration by external impetus, mode is flexible, and adaptability is good.
(5) heat supply temperature can be improved by a relatively large margin, compensate for the deficiency of absorption heat pump technology, and avoid driving thermal medium ginseng
Number and conflicting between solution property.
(6) as heat pump, it is possible to directly utilize surrounding air as low-temperature heat source, and not by temperature limiting；Solve absorption
Heat pump is about the source of low-temperature heat source and a temperature limiting difficult problem.
(7) rely primarily on latent heat and realize acquisition and the release of thermic load, overcome the deficiency of gas compression formula heat pump techniques.
(8) multiple concrete technical scheme is provided, it is possible to tackle numerous different actual state, have the wider scope of application.
(9) extend heat pump techniques, enrich the type of compression heat pump, be conducive to being better achieved the efficient utilization of heat energy.
Claims (18)
1. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, choke valve,
Solution pump, solution heat exchanger, compressor, the second compressor, decompressor and high-temperature heat exchanger are formed；Absorber (1)
Having weak solution pipeline to connect with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2) is the denseest
Solution line connects with absorber (1) through solution heat exchanger (7), and generator (2) also has refrigerant steam channel and condenser
(3) connection, condenser (3) also has cryogen liquid pipeline to connect with vaporizer (4) through cold choke valve (5), vaporizer (4)
Also having refrigerant steam channel to connect with absorber (1), outside has low-temperature heat medium passage to connect with compressor (8), compressor
(8) also having low-temperature heat medium passage to connect with the second compressor (9) through vaporizer (4), the second compressor (9) is the lowest
Warm passage connects with decompressor (10) through high-temperature heat exchanger (11), and decompressor (10) also has low-temperature heat medium to lead to
Road and ft connection, generator (2) and high-temperature heat exchanger (11) have high temperature thermal medium passage and ft connection the most respectively, inhale
Receiving device (1) and condenser (3) has heated medium passage and ft connection the most respectively, decompressor (10) connects compressor (8)
With the second compressor (9) transmit power, form first kind thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (10)
Connect compressor (8), the second compressor (9) and solution pump (6) and transmit power.
2. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, choke valve,
Solution pump, solution heat exchanger, compressor, the second compressor, decompressor, high-temperature heat exchanger and the 3rd compressor are formed；
Absorber (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (7) through solution pump (6), generator
(2) also having concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), generator (2) also has refrigerant vapour
Passage connects with condenser (3), and condenser (3) also has cryogen liquid pipeline to connect with vaporizer (4) through cold choke valve (5),
Vaporizer (4) also has refrigerant steam channel to connect with absorber (1), and there are low-temperature heat medium passage and the 3rd compressor (12) in outside
Connection, the 3rd compressor (12) also has low-temperature heat medium passage to connect with compressor (8) through vaporizer (4), compressor (8)
Also having low-temperature heat medium passage to connect with the second compressor (9) through vaporizer (4), the second compressor (9) also has Low Temperature Thermal to be situated between
Matter passage connects with decompressor (10) through high-temperature heat exchanger (11), and decompressor (10) also has low-temperature heat medium passage with outer
Portion connects, and generator (2) and high-temperature heat exchanger (11) have high temperature thermal medium passage and ft connection, absorber (1) the most respectively
Having heated medium passage and ft connection the most respectively with condenser (3), decompressor (10) connects compressor (8), the second pressure
Contracting machine (9) and the 3rd compressor (12) also transmit power, form first kind thermal drivers compressing-absorbing type heat pump；Wherein, or
Decompressor (10) connects compressor (8), the second compressor (9), the 3rd compressor (12) and solution pump (6) and transmits dynamic
Power.
3. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, choke valve,
Solution pump, solution heat exchanger, compressor, the second compressor, decompressor, high-temperature heat exchanger, the 3rd compressor and second
High-temperature heat exchanger is formed；Absorber (1) has weak solution pipeline through solution pump (6) and solution heat exchanger (7) and to occur
Device (2) connects, and generator (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), occurs
Device (2) also has refrigerant steam channel to connect with condenser (3), and condenser (3) also has cryogen liquid pipeline through cold choke valve (5)
Connecting with vaporizer (4), vaporizer (4) also has refrigerant steam channel to connect with absorber (1), and there is low-temperature heat medium outside
Passage connects with compressor (8), and compressor (8) also has low-temperature heat medium passage through vaporizer (4) and the second compressor (9)
Connection, the second compressor (9) also has low-temperature heat medium passage to connect with the 3rd compressor (12) through high-temperature heat exchanger (11),
3rd compressor (12) also has low-temperature heat medium passage to connect with decompressor (10) through the second high-temperature heat exchanger (13), swollen
Swollen machine (10) also has low-temperature heat medium passage and ft connection, generator (2), high-temperature heat exchanger (11) and the second high temperature
Heat exchanger (13) has high temperature thermal medium passage and ft connection, absorber (1) and condenser (3) to have the most respectively the most respectively
Heated medium passage and ft connection, decompressor (10) connects compressor (8), the second compressor (9) and the 3rd compressor
(12) and transmit power, first kind thermal drivers compressing-absorbing type heat pump is formed；Wherein, or decompressor (10) connect compressor
(8), the second compressor (9), the 3rd compressor (12) and solution pump (6) transmit power.
4. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, choke valve,
Solution pump, solution heat exchanger, compressor, the second compressor, decompressor, high-temperature heat exchanger, the second decompressor and second
High-temperature heat exchanger is formed；Absorber (1) has weak solution pipeline through solution pump (6) and solution heat exchanger (7) and to occur
Device (2) connects, and generator (2) also has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7), occurs
Device (2) also has refrigerant steam channel to connect with condenser (3), and condenser (3) also has cryogen liquid pipeline through cold choke valve (5)
Connecting with vaporizer (4), vaporizer (4) also has refrigerant steam channel to connect with absorber (1), and there is low-temperature heat medium outside
Passage connects with compressor (8), and compressor (8) also has low-temperature heat medium passage through vaporizer (4) and the second compressor (9)
Connection, the second compressor (9) also has low-temperature heat medium passage to connect with the second decompressor (14) through high-temperature heat exchanger (11),
Second decompressor (14) also has low-temperature heat medium passage to connect with decompressor (10) through the second high-temperature heat exchanger (13), swollen
Swollen machine (10) also has low-temperature heat medium passage and ft connection, generator (2), high-temperature heat exchanger (11) and the second high temperature
Heat exchanger (13) has high temperature thermal medium passage and ft connection, absorber (1) and condenser (3) to have the most respectively the most respectively
Heated medium passage and ft connection, decompressor (10) and the second decompressor (14) connect compressor (8) and the second compression
Machine (9) also transmits power, forms first kind thermal drivers compressing-absorbing type heat pump；Wherein, or decompressor (10) and second swollen
Swollen machine (14) connects compressor (8), the second compressor (9) and solution pump (6) and transmits power.
5. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, choke valve,
Solution pump, solution heat exchanger, compressor, the second compressor, decompressor, high-temperature heat exchanger and regenerator are formed；Inhale
Receiving device (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2)
Also have concentrated solution pipeline connect with absorber (1) through solution heat exchanger (7), generator (2) also refrigerant steam channel and
Condenser (3) connects, and condenser (3) also has cryogen liquid pipeline to connect with vaporizer (4) through cold choke valve (5), evaporation
Device (4) also has refrigerant steam channel to connect with absorber (1), and outside has low-temperature heat medium passage to connect with compressor (8),
Compressor (8) also has low-temperature heat medium passage to connect with the second compressor (9) with vaporizer (4) through regenerator (15), the
Two compressors (9) also have low-temperature heat medium passage to connect with decompressor (10) through regenerator (15) and high-temperature heat exchanger (11)
Logical, decompressor (10) also has low-temperature heat medium passage and ft connection, and generator (2) and high-temperature heat exchanger (11) also divide
High temperature thermal medium passage and ft connection, absorber (1) and condenser (3) is not had to have heated medium passage the most respectively with outer
Portion connects, and decompressor (10) connects compressor (8) and the second compressor (9) and transmits power, forms first kind thermal drivers
Compressing-absorbing type heat pump；Wherein, or decompressor (10) connects compressor (8), the second compressor (9) and solution pump (6)
And transmit power.
6. first kind thermal drivers compressing-absorbing type heat pump, mainly by absorber, generator, condenser, vaporizer, choke valve,
Solution pump, solution heat exchanger, compressor, the second compressor, decompressor, high-temperature heat exchanger and regenerator are formed；Inhale
Receiving device (1) has weak solution pipeline to connect with generator (2) with solution heat exchanger (7) through solution pump (6), generator (2)
Also have concentrated solution pipeline connect with absorber (1) through solution heat exchanger (7), generator (2) also refrigerant steam channel and
Condenser (3) connects, and condenser (3) also has cryogen liquid pipeline to connect with vaporizer (4) through cold choke valve (5), evaporation
Device (4) also has refrigerant steam channel to connect with absorber (1), and there is low-temperature heat medium passage outside through regenerator (15) and pressure
Contracting machine (8) connects, and compressor (8) also has low-temperature heat medium passage to compress with second through vaporizer (4) and regenerator (15)
Machine (9) connects, and the second compressor (9) also has low-temperature heat medium passage through high-temperature heat exchanger (11) and decompressor (10)
Connection, decompressor (10) also has low-temperature heat medium passage and ft connection, generator (2) and high-temperature heat exchanger (11) also
Have respectively high temperature thermal medium passage and ft connection, absorber (1) and condenser (3) have the most respectively heated medium passage with
Ft connection, decompressor (10) connects compressor (8) and the second compressor (9) and transmits power, forms first kind heat and drives
Dynamic pressure contracting-absorption heat pump；Wherein, or decompressor (10) connects compressor (8), the second compressor (9) and solution pump (6)
And transmit power.
7. first kind thermal drivers compressing-absorbing type heat pump, is in arbitrary first kind thermal drivers compression-absorption described in claim 1-6
Formula heat pump, increases the second generator, second throttle, the second solution pump and the second solution heat exchanger, and absorber (1) is set up
Weak solution pipeline connects with the second generator (16) with the second solution heat exchanger (19) through the second solution pump (18), and second
Generator (16) also has concentrated solution pipeline to connect with absorber (1) through the second solution heat exchanger (19), by generator (2)
Have refrigerant steam channel to connect with condenser (3) to be adjusted to generator (2) and have refrigerant steam channel and the second generator (16)
After connection, the second generator (16) has cryogen liquid pipeline to connect with condenser (3) through second throttle (17) again, second
Raw device (16) also has refrigerant steam channel to connect with condenser (4), forms first kind thermal drivers compressing-absorbing type heat pump.
8. first kind thermal drivers compressing-absorbing type heat pump, is in arbitrary first kind thermal drivers compression-absorption described in claim 1-6
Formula heat pump, increases the second generator, second throttle and the second solution heat exchanger, and absorber (1) is had weak solution pipeline warp
Solution pump (6) and solution heat exchanger (7) connect with generator (2) and are adjusted to absorber (1) and have weak solution pipeline through molten
Liquid pump (6), solution heat exchanger (7) connect with generator (2) with the second solution heat exchanger (19), by generator (2)
Have concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7) to be adjusted to generator (2) and have concentrated solution pipeline through
Two solution heat exchangers (19) connect with the second generator (16), and the second generator (16) has concentrated solution pipeline again through solution
Heat exchanger (7) connects with absorber (1), has refrigerant steam channel to connect adjustment with condenser (3) in generator (2)
After having refrigerant steam channel to connect with the second generator (16) for generator (2), the second generator (16) has cryogen liquid pipe again
Road connects with condenser (3) through second throttle (17), and the second generator (16) also has refrigerant steam channel and condenser (3)
Connection, forms first kind thermal drivers compressing-absorbing type heat pump.
9. first kind thermal drivers compressing-absorbing type heat pump, is in arbitrary first kind thermal drivers compression-absorption described in claim 1-6
Formula heat pump, increases the second generator, second throttle, the second solution pump and the second solution heat exchanger, is had by absorber (1)
Weak solution pipeline connects with generator (2) through solution pump (6) and solution heat exchanger (7) and is adjusted to absorber (1) and has dilute
Solution line connects with the second generator (16) with solution heat exchanger (7) through solution pump (6), the second generator (16)
There is concentrated solution pipeline to connect with generator (2) with the second solution heat exchanger (19) through the second solution pump (18) again, will occur
Device (2) has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7) to be adjusted to generator (2) and have concentrated solution
Pipeline connects with absorber (1) with solution heat exchanger (7) through the second solution heat exchanger (19), is had by generator (2)
Refrigerant steam channel connects with condenser (3) and is adjusted to generator (2) and has refrigerant steam channel and the second generator (16) even
After Tong, the second generator (16) has cryogen liquid pipeline to connect with condenser (3) through second throttle (17) again, and second occurs
Device (16) also has refrigerant steam channel to connect with condenser (3), forms first kind thermal drivers compressing-absorbing type heat pump.
10. first kind thermal drivers compressing-absorbing type heat pump, is in arbitrary first kind thermal drivers compression-suction described in claim 1-6
Receipts formula heat pump, increases the second generator, the second absorber, the second solution pump and the second solution heat exchanger, by absorber (1)
Have weak solution pipeline to connect with generator (2) through solution pump (6) and solution heat exchanger (7) to be adjusted to absorber (1) and have
Weak solution pipeline connects with the second absorber (20) with solution heat exchanger (7) through solution pump (6), the second absorber (20)
There is weak solution pipeline to connect with generator (2) with the second solution heat exchanger (19) through the second solution pump (18) again, will occur
Device (2) has concentrated solution pipeline to connect with absorber (1) through solution heat exchanger (7) to be adjusted to generator (2) and have concentrated solution
Pipeline connects with the second generator (16) through the second solution heat exchanger (19), and the second generator (16) has concentrated solution pipe again
Road connects with absorber (1) through solution heat exchanger (7), and the second generator (16) also has refrigerant steam channel to inhale with second
Receiving device (20) connection, the second generator (16) also has high temperature thermal medium passage and ft connection, and the second absorber (20) is also
There are heated medium passage and ft connection, form first kind thermal drivers compressing-absorbing type heat pump.
11. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-absorption described in claim 10
Formula heat pump, increases the 3rd generator, second throttle, the 3rd solution pump and the 3rd solution heat exchanger, the second absorber (20)
Set up weak solution pipeline to connect with the 3rd generator (21) with the 3rd solution heat exchanger (23) through the 3rd solution pump (22),
3rd generator (21) also has concentrated solution pipeline to connect with the second generator (16) through the 3rd solution heat exchanger (23), will
Generator (2) have refrigerant steam channel connect with condenser (3) be adjusted to generator (2) have refrigerant steam channel with the 3rd
After raw device (21) connection, the 3rd generator (21) has cryogen liquid pipeline through second throttle (17) with condenser (3) even again
Logical, the 3rd generator (21) also has refrigerant steam channel to connect with condenser (3), forms first kind thermal drivers compression-absorption
Formula heat pump.
12. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-absorption described in claim 10
Formula heat pump, increases the 3rd generator, second throttle and the 3rd solution heat exchanger, the second absorber (20) is had weak solution
Pipeline connects with generator (2) through the second solution pump (18) and the second solution heat exchanger (19) and is adjusted to the second absorber (20)
Weak solution pipeline is had through the second solution pump (18), the second solution heat exchanger (19) and the 3rd solution heat exchanger (23) and to send out
Raw device (2) connection, has concentrated solution pipeline through the second solution heat exchanger (19) and the second generator (16) by generator (2)
Connection is adjusted to generator (2) has concentrated solution pipeline to connect with the 3rd generator (21) through the 3rd solution heat exchanger (23),
3rd generator (21) has concentrated solution pipeline to connect with the second generator (16) through the second solution heat exchanger (19) again, will
Generator (2) have refrigerant steam channel connect with condenser (3) be adjusted to generator (2) have refrigerant steam channel with the 3rd
After raw device (21) connection, the 3rd generator (21) has cryogen liquid pipeline through second throttle (17) with condenser (3) even again
Logical, the 3rd generator (21) also has refrigerant steam channel to connect with condenser (3), forms first kind thermal drivers compression-absorption
Formula heat pump.
13. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-absorption described in claim 10
Formula heat pump, increases the 3rd generator, second throttle, the 3rd solution pump and the 3rd solution heat exchanger, by the second absorber (20)
There is weak solution pipeline to connect with generator (2) through the second solution pump (18) and the second solution heat exchanger (19) and be adjusted to second
Absorber (20) has weak solution pipeline through the second solution pump (18) and the second solution heat exchanger (19) and the 3rd generator (21)
Connection, the 3rd generator (21) have concentrated solution pipeline through the 3rd solution pump (22) and the 3rd solution heat exchanger (23) again and
Generator (2) connects, and generator (2) has concentrated solution pipeline through the second solution heat exchanger (19) and the second generator (16)
Connection is adjusted to generator (2) has concentrated solution pipeline through the 3rd solution heat exchanger (23) and the second solution heat exchanger (19)
Connect with the second generator (16), generator (2) has refrigerant steam channel connect with condenser (3) and is adjusted to generator
(2) after having refrigerant steam channel to connect with the 3rd generator (21), the 3rd generator (21) has cryogen liquid pipeline again through second
Choke valve (17) connects with condenser (3), and the 3rd generator (21) also has refrigerant steam channel to connect with condenser (3),
Form first kind thermal drivers compressing-absorbing type heat pump.
14. first kind thermal drivers compressing-absorbing type heat pumps, are in claim 1-6, arbitrary first kind thermal drivers pressure described in 10
In contracting-absorption heat pump, increase newly-increased generator, newly-increased absorber, new solubilization liquid pump and newly-increased solution heat exchanger, will occur
Device (2) has refrigerant steam channel to connect with condenser (3) to be adjusted to generator (2) and have refrigerant steam channel and newly-increased absorber
(B) connection, newly-increased absorber (B) also has weak solution pipeline through new solubilization liquid pump (C) and newly-increased solution heat exchanger (D)
Connecting with newly-increased generator (A), newly-increased generator (A) also has concentrated solution pipeline through newly-increased solution heat exchanger (D) with newly-increased
Absorber (B) connects, and newly-increased generator (A) also has refrigerant steam channel to connect with condenser (3), newly-increased generator (A)
Also have high temperature thermal medium passage and ft connection, newly-increased absorber (B) to also have heated medium passage and ft connection, form the
One class thermal drivers compressing-absorbing type heat pump.
15. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-suction described in claim 7-9
In receipts formula heat pump, the second generator (16) sets up high temperature thermal medium passage and ft connection, forms first kind thermal drivers compression-suction
Receipts formula heat pump.
16. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-suction described in claim 11-13
In receipts formula heat pump, the 3rd generator (21) sets up high temperature thermal medium passage and ft connection, forms first kind thermal drivers compression-suction
Receipts formula heat pump.
17. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-suction described in claim 1-16
In receipts formula heat pump, increasing engine, engine (24) connects compressor (8) and transmits power to compressor (8), is formed
Additional external power-actuated first kind thermal drivers compressing-absorbing type heat pump.
18. first kind thermal drivers compressing-absorbing type heat pumps, are in arbitrary first kind thermal drivers compression-suction described in claim 1-16
In receipts formula heat pump, increasing working machine, decompressor (10) connects working machine (25) and transmits power, shape to working machine (25)
Become the additional first kind thermal drivers compressing-absorbing type heat pump that living load is externally provided.
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1128856A (en) * | 1994-09-27 | 1996-08-14 | 巴布考克及威尔考克斯公司 | Ammonia absorption circulation used for combined circulation power apparatus |
| JP2000193341A (en) * | 1998-12-25 | 2000-07-14 | Takenaka Komuten Co Ltd | Ice making system |
| CN1804511A (en) * | 2006-01-23 | 2006-07-19 | 李华玉 | Compression-absorption combined heat pump heating system |
| CN103743150A (en) * | 2013-12-17 | 2014-04-23 | 浙江理工大学 | Absorption compression type automatic-overlapping refrigerating system and use method |
| CN104236160A (en) * | 2013-06-13 | 2014-12-24 | 彭岫麟 | Hybrid system combining cooling device and absorption heat pump |
-
2016
- 2016-04-11 CN CN201610243933.2A patent/CN105823265B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1128856A (en) * | 1994-09-27 | 1996-08-14 | 巴布考克及威尔考克斯公司 | Ammonia absorption circulation used for combined circulation power apparatus |
| JP2000193341A (en) * | 1998-12-25 | 2000-07-14 | Takenaka Komuten Co Ltd | Ice making system |
| CN1804511A (en) * | 2006-01-23 | 2006-07-19 | 李华玉 | Compression-absorption combined heat pump heating system |
| CN104236160A (en) * | 2013-06-13 | 2014-12-24 | 彭岫麟 | Hybrid system combining cooling device and absorption heat pump |
| CN103743150A (en) * | 2013-12-17 | 2014-04-23 | 浙江理工大学 | Absorption compression type automatic-overlapping refrigerating system and use method |
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